CN110317656A - A kind of paper plant's bottom ash regeneration manufacture at biomass fuel technique - Google Patents
A kind of paper plant's bottom ash regeneration manufacture at biomass fuel technique Download PDFInfo
- Publication number
- CN110317656A CN110317656A CN201910705476.8A CN201910705476A CN110317656A CN 110317656 A CN110317656 A CN 110317656A CN 201910705476 A CN201910705476 A CN 201910705476A CN 110317656 A CN110317656 A CN 110317656A
- Authority
- CN
- China
- Prior art keywords
- bottom ash
- biomass fuel
- machine
- product
- ash material
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L5/00—Solid fuels
- C10L5/40—Solid fuels essentially based on materials of non-mineral origin
- C10L5/48—Solid fuels essentially based on materials of non-mineral origin on industrial residues and waste materials
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/08—Drying or removing water
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/10—Recycling of a stream within the process or apparatus to reuse elsewhere therein
-
- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10L—FUELS NOT OTHERWISE PROVIDED FOR; NATURAL GAS; SYNTHETIC NATURAL GAS OBTAINED BY PROCESSES NOT COVERED BY SUBCLASSES C10G, C10K; LIQUEFIED PETROLEUM GAS; ADDING MATERIALS TO FUELS OR FIRES TO REDUCE SMOKE OR UNDESIRABLE DEPOSITS OR TO FACILITATE SOOT REMOVAL; FIRELIGHTERS
- C10L2290/00—Fuel preparation or upgrading, processes or apparatus therefore, comprising specific process steps or apparatus units
- C10L2290/40—Applying a magnetic field or inclusion of magnets in the apparatus
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
Landscapes
- Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Organic Chemistry (AREA)
- Solid Fuels And Fuel-Associated Substances (AREA)
Abstract
The invention discloses a kind of paper plant's bottom ash regeneration manufactures into the technique of biomass fuel, comprising the following steps: extruding magnetic separation, tears up, dries, being crushed, selection by winnowing, molding, packaging;This technique is realized by the method for pure physics to the metal recovery and the utilization of resources in waste residue.On the one hand metal material is sub-elected by magnetic separation and vortex, realizes the recycling of resource;On the other hand, remaining waste materials are fabricated to biomass fuel by crushing and forming, realize the regeneration of resource.
Description
Technical field
The present invention relates to refuse reclamation technical field, especially a kind of paper plant's bottom ash regeneration manufacture is at biomass fuel
The technique of material.
Background technique
Pulping and paper-making raw material is needed by washing impurity-removing, if timber and non-wood fiber melting process are to wood chip, reed piece and grass
After the raw materials such as piece are washed, the biomass waste residues such as a large amount of sawdusts, reed slag and dust can be generated.These impurity are more and more, at
For a great problem for polluting environment.There are two types of the waste sludge from paper mill isolated in production process: one is dry method except the waste residue gone out, is
Some light dust are in the majority, and water content is not high, but use value is lower.Another kind is that wet process removes waste residue out, water content
Very up to saturation, it is necessary to carrying out high-efficiency dehydration drying and other treatment could efficiently use, this kind of impurity after drying and other treatment calorific value compared with
Height has higher reclamation utility value.The calorific value of general 2 tons of over dry waste residues is suitable with 1 ton of standard coal, and energy-saving benefit is very
It is considerable.
Biomass molding fuel is because of its special synthesis technology and is widely applied field and has been to be concerned by more and more people,
Its investigative technique also will be important topic that Chinese future development biomass energy is faced.Paper mill utilizes regrown material papermaking
When, a large amount of waste material, including twisted rope, secondary stock, waste plastics etc. can be generated in production process, the processing for these waste materials is existing
They cannot be carried out classification recycling well by some treatment process.
Existing technology is that the bottom ash that paper mill is generated passes through the method for washing, light plastic and the paper pulp of remnants
It sorts out.Remaining waste residue just passes through the method processing of landfill and burning.This processing method for paper plant's waste residue, a side
Face can not recycle the metal material in waste residue, waste of resource;On the other hand, only after simply sorting, residue is useless
Slag is filled and is burned, and is wasted the resource in waste residue, also be polluted environment.
Summary of the invention
It is an object of the invention to overcome existing to be easy to cause resource waste and pollution for paper plant's Solid state fermentation technology
The problem of environment, provides a kind of paper plant's bottom ash regeneration manufacture into the technique of biomass fuel.
A kind of paper plant's bottom ash regeneration manufacture at biomass fuel technique, comprising the following steps:
S1: squeezing: the bottom ash material containing moisture content being poured into extruder and is squeezed, and squeeze to bottom ash material and remove
Water, so that the moisture content of bottom ash material is reduced to 50% hereinafter, obtaining bottom ash material A;
S2: magnetic separation: the bottom ash material A in S1 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, so
After obtain bottom ash material B;
S3: it tears up: the bottom ash material B in S2 is poured into shredder, shredder tears up bottom ash material B, then obtains thin
Expect A;
S4: secondary magnetic separation: the fines A in S3 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, then
Obtain fines B;
S5: drying: the fines B in S4 is put into dryer and is dried, obtains dry and hard piece;
S6: broken: dry and hard piece in S5 being put into crusher and is crushed, product A is obtained;
S7: selection by winnowing: the product A in S6 is put into winnowing machine and carries out metal sorting, obtains other metal charges and product B:
S8: magnetic separation three times: the product B in S7 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, then
Obtain product C;
S9: molding: the product C in S8 is put into molding machine, is formed, obtains biomass fuel;
S10: the biomass fuel in S8 packaging: is subjected to quantitative package.
Further, a kind of paper plant's bottom ash regeneration according to claim 1 manufactures the work at biomass fuel
Skill, it is characterised in that: shredder edge of a knife quantity is set as 24 knives in the S3.
Further, the crusher edge of a knife quantity is set as 12 knives.
Further, the temperature control of the dryer is 180 DEG C~220 DEG C.
The beneficial effects of the present invention are: method of this technique by pure physics, is realized to the metal recovery and money in waste residue
Source utilizes.On the one hand metal material is sub-elected by magnetic separation and whirlpool selection by winnowing, realizes the recycling of resource;On the other hand, pass through powder
Remaining waste materials are fabricated to biomass fuel by broken and molding, realize the regeneration of resource.
Specific embodiment
Illustrate embodiments of the present invention below by way of specific specific example, those skilled in the art can be by this specification
Other advantages and efficacy of the present invention can be easily understood for disclosed content.The present invention can also pass through in addition different specific realities
The mode of applying is embodied or practiced, the various details in this specification can also based on different viewpoints and application, without departing from
Various modifications or alterations are carried out under spirit of the invention.It should be noted that in the absence of conflict, following embodiment and implementation
Feature in example can be combined with each other.
Embodiment 1:
A kind of paper plant's bottom ash regeneration manufacture at biomass fuel technique, comprising the following steps:
S1: squeezing: the bottom ash material containing moisture content being poured into extruder and is squeezed, and squeeze to bottom ash material and remove
Water, so that the moisture content of bottom ash material is reduced to 50% hereinafter, obtaining bottom ash material A;
S2: magnetic separation: the bottom ash material A in S1 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, so
After obtain bottom ash material B;100 type of Ferromagnet machine model, the magnet drum revolving speed in Ferromagnet machine are 60r/s.
S3: it tears up: the bottom ash material B in S2 is poured into shredder, shredder tears up bottom ash material B, then obtains thin
Expect A;1200 type of shredder model, shredder edge of a knife quantity are set as 24 knives, and revolving speed control is 60r/s.
S4: secondary magnetic separation: the fines A in S3 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, then
Obtain fines B;100 type of Ferromagnet machine model, the magnet drum revolving speed in Ferromagnet machine are 60r/s.
S5: drying: the fines B in S4 is put into dryer and is dried, obtains dry and hard piece;The dryer model 15
The temperature control of type, dryer is 180 DEG C.
S6: broken: dry and hard piece in S5 being put into crusher and is crushed, product A is obtained;The crusher uses 70
Type, crusher edge of a knife quantity are set as 12 knives, and revolving speed control is 600r/s.
S7: selection by winnowing: the product A in S6 is put into winnowing machine and carries out metal sorting, obtains other metal charges and product B: institute
Stating the control of winnowing machine revolving speed is 60r/s.
S8: magnetic separation three times: the product B in S7 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, then
Obtain product C;100 type of Ferromagnet machine model, the magnet drum revolving speed in Ferromagnet machine are 60r/s.
S9: molding: the product C in S8 is put into molding machine, is formed, obtains biomass fuel;The molding machine
Using 730 type molding machines, molding port egress aperture compression ratio 6:1.The diameter of the biomass fuel is 7.5mm, length
For 19.5mm.
S10: the biomass fuel in S8 packaging: is subjected to 25kg quantitative package.
The water content of the bottom ash material used is 70% or so, and iron-content is 5% or so, paper pulp 20% or so, and plastics 4% are left
The right side, other 1% or so.3.5 tons of bottom ash material can be produced into 1000kg fuel by this technique, select the iron of 10kg.
Embodiment 2:
A kind of paper plant's bottom ash regeneration manufacture at biomass fuel technique, comprising the following steps:
S1: squeezing: the bottom ash material containing moisture content being poured into extruder and is squeezed, and squeeze to bottom ash material and remove
Water, so that the moisture content of bottom ash material is reduced to 50% hereinafter, obtaining bottom ash material A;
S2: magnetic separation: the bottom ash material A in S1 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, so
After obtain bottom ash material B;100 type of Ferromagnet machine model, the magnet drum revolving speed in Ferromagnet machine are 60r/s.
S3: it tears up: the bottom ash material B in S2 is poured into shredder, shredder tears up bottom ash material B, then obtains thin
Expect A;1200 type of shredder model, shredder edge of a knife quantity are set as 24 knives, and revolving speed control is 60r/s.
S4: secondary magnetic separation: the fines A in S3 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, then
Obtain fines B;100 type of Ferromagnet machine model, the magnet drum revolving speed in Ferromagnet machine are 60r/s.
S5: drying: the fines B in S4 is put into dryer and is dried, obtains dry and hard piece;The dryer model 15
The temperature control of type, dryer is 200 DEG C.
S6: broken: dry and hard piece in S5 being put into crusher and is crushed, product A is obtained;The crusher uses 70
Type, crusher edge of a knife quantity are set as 12 knives, and revolving speed control is 600r/s.
S7: selection by winnowing: the product A in S6 is put into winnowing machine and carries out metal sorting, obtains other metal charges and product B: institute
Stating the control of winnowing machine revolving speed is 60r/s.
S8: magnetic separation three times: the product B in S7 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, then
Obtain product C;100 type of Ferromagnet machine model, the magnet drum revolving speed in Ferromagnet machine are 60r/s.
S9: molding: the product C in S8 is put into molding machine, is formed, obtains biomass fuel;The molding machine
Using 730 type molding machines, molding port egress aperture compression ratio 6:1.The diameter of the biomass fuel is 8mm, and length is
20mm。
S10: the biomass fuel in S8 packaging: is subjected to 25kg quantitative package.
The water content of the bottom ash material used is 70% or so, and iron-content is 5% or so, paper pulp 20% or so, and plastics 4% are left
The right side, other 1% or so.3.5 tons of bottom ash material can be produced into 990kg fuel by this technique, select the iron of 11kg.
Embodiment 3:
A kind of paper plant's bottom ash regeneration manufacture at biomass fuel technique, comprising the following steps:
S1: squeezing: the bottom ash material containing moisture content being poured into extruder and is squeezed, and squeeze to bottom ash material and remove
Water, so that the moisture content of bottom ash material is reduced to 50% hereinafter, obtaining bottom ash material A;
S2: magnetic separation: the bottom ash material A in S1 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, so
After obtain bottom ash material B;100 type of Ferromagnet machine model, the magnet drum revolving speed in Ferromagnet machine are 60r/s.
S3: it tears up: the bottom ash material B in S2 is poured into shredder, shredder tears up bottom ash material B, then obtains thin
Expect A;1200 type of shredder model, shredder edge of a knife quantity are set as 24 knives, and revolving speed control is 60r/s.
S4: secondary magnetic separation: the fines A in S3 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, then
Obtain fines B;100 type of Ferromagnet machine model, the magnet drum revolving speed in Ferromagnet machine are 60r/s.
S5: drying: the fines B in S4 is put into dryer and is dried, obtains dry and hard piece;The dryer model 15
The temperature control of type, dryer is 220 DEG C.
S6: broken: dry and hard piece in S5 being put into crusher and is crushed, product A is obtained;The crusher uses 70
Type, crusher edge of a knife quantity are set as 12 knives, and revolving speed control is 600r/s.
S7: selection by winnowing: the product A in S6 is put into winnowing machine and carries out metal sorting, obtains other metal charges and product B: institute
Stating the control of winnowing machine revolving speed is 60r/s.
S8: magnetic separation three times: the product B in S7 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, then
Obtain product C;100 type of Ferromagnet machine model, the magnet drum revolving speed in Ferromagnet machine are 60r/s.
S9: molding: the product C in S8 is put into molding machine, is formed, obtains biomass fuel;The molding machine
Using 730 type molding machines, molding port egress aperture compression ratio 6:1.The diameter of the biomass fuel is 8.5mm, length
For 20mm.
S10: the biomass fuel in S8 packaging: is subjected to 25kg quantitative package.
The water content of the bottom ash material used is 70% or so, and iron-content is 5% or so, paper pulp 20% or so, and plastics 4% are left
The right side, other 1% or so.3.5 tons of bottom ash material can be produced into 1020kg fuel by this technique, select the iron of 8kg.
A specific embodiment of the invention above described embodiment only expresses, the description thereof is more specific and detailed, but simultaneously
Limitations on the scope of the patent of the present invention therefore cannot be interpreted as.It should be pointed out that for those of ordinary skill in the art
For, without departing from the inventive concept of the premise, various modifications and improvements can be made, these belong to guarantor of the invention
Protect range.
Claims (4)
1. a kind of paper plant's bottom ash regeneration manufacture is at the technique of biomass fuel, it is characterised in that: the following steps are included:
S1: it squeezes: the bottom ash material containing moisture content being poured into extruder and is squeezed, extruding water removal is carried out to bottom ash material, is made
The moisture content for obtaining bottom ash material is reduced to 50% hereinafter, obtaining bottom ash material A;
S2: magnetic separation: the bottom ash material A in S1 is uniformly placed on above Ferromagnet machine, sorts tapping by Ferromagnet machine, then
Slag charge B on earth;
S3: it tears up: the bottom ash material B in S2 being poured into shredder, shredder tears up bottom ash material B, then obtains fines A;
S4: secondary magnetic separation: the fines A in S3 is uniformly placed on above Ferromagnet machine, is sorted tapping by Ferromagnet machine, is then obtained
Fines B;
S5: drying: the fines B in S4 is put into dryer and is dried, obtains dry and hard piece;
S6: broken: dry and hard piece in S5 being put into crusher and is crushed, product A is obtained;
S7: selection by winnowing: the product A in S6 is put into winnowing machine and carries out metal sorting, obtains other metal charges and product B:
S8: magnetic separation three times: the product B in S7 is uniformly placed on above Ferromagnet machine, is sorted tapping by Ferromagnet machine, is then obtained
Product C;
S9: molding: the product C in S8 is put into molding machine, is formed, obtains biomass fuel;
S10: the biomass fuel in S8 packaging: is subjected to quantitative package.
2. a kind of paper plant's bottom ash regeneration manufacture according to claim 1 exists at the technique of biomass fuel, feature
In: shredder edge of a knife quantity is set as 24 knives in the S3.
3. a kind of paper plant's bottom ash regeneration manufacture according to claim 1 exists at the technique of biomass fuel, feature
In: the crusher edge of a knife quantity is set as 12 knives.
4. a kind of paper plant's bottom ash regeneration manufacture according to claim 1 exists at the technique of biomass fuel, feature
In: the temperature control of the dryer is 180 DEG C~220 DEG C.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910705476.8A CN110317656A (en) | 2019-08-01 | 2019-08-01 | A kind of paper plant's bottom ash regeneration manufacture at biomass fuel technique |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201910705476.8A CN110317656A (en) | 2019-08-01 | 2019-08-01 | A kind of paper plant's bottom ash regeneration manufacture at biomass fuel technique |
Publications (1)
Publication Number | Publication Date |
---|---|
CN110317656A true CN110317656A (en) | 2019-10-11 |
Family
ID=68125269
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201910705476.8A Pending CN110317656A (en) | 2019-08-01 | 2019-08-01 | A kind of paper plant's bottom ash regeneration manufacture at biomass fuel technique |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110317656A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111375479A (en) * | 2020-04-14 | 2020-07-07 | 浙江山鹰纸业有限公司 | Bottom slag sorting process and equipment thereof |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1834340A (en) * | 2005-03-18 | 2006-09-20 | 曾碚凯 | Separating method and system for waste paper and waste plastic mixture |
CN102671922A (en) * | 2012-05-28 | 2012-09-19 | 东莞地龙纸业有限公司 | Method for recycling papermaking waste residues |
CN108342239A (en) * | 2017-01-25 | 2018-07-31 | 无锡荣成环保科技有限公司 | The method that fuel rod is made using the slag charge of reclaimed waste paper |
CN109465280A (en) * | 2018-12-21 | 2019-03-15 | 中山斯瑞德环保科技有限公司 | Equipment and method for preparing RDF-5 by using paper mill stranded rope |
-
2019
- 2019-08-01 CN CN201910705476.8A patent/CN110317656A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN1834340A (en) * | 2005-03-18 | 2006-09-20 | 曾碚凯 | Separating method and system for waste paper and waste plastic mixture |
CN102671922A (en) * | 2012-05-28 | 2012-09-19 | 东莞地龙纸业有限公司 | Method for recycling papermaking waste residues |
CN108342239A (en) * | 2017-01-25 | 2018-07-31 | 无锡荣成环保科技有限公司 | The method that fuel rod is made using the slag charge of reclaimed waste paper |
CN109465280A (en) * | 2018-12-21 | 2019-03-15 | 中山斯瑞德环保科技有限公司 | Equipment and method for preparing RDF-5 by using paper mill stranded rope |
Non-Patent Citations (1)
Title |
---|
张鸿郭等: "《固体废物处理与资源化实验教程》", 31 January 2018, 北京理工大学出版社 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN111375479A (en) * | 2020-04-14 | 2020-07-07 | 浙江山鹰纸业有限公司 | Bottom slag sorting process and equipment thereof |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN201917184U (en) | Dehydration drying system for Chinese medicine dregs | |
IE59804B1 (en) | Process and device for working up household, industrial and other similar waste | |
AU2016366642B2 (en) | Waste processing | |
CN103861863B (en) | A kind of domestic waste Comprehensive utilization method | |
CN102041127A (en) | Preparation method for preparing derived fuel by utilizing combustible materials in garbage | |
CN105268723A (en) | Papermaking solid waste treatment method | |
CN109435107A (en) | A kind of recycling waste plastic process system | |
CN102357942A (en) | Production method for recycled bottle sheet | |
CN110317656A (en) | A kind of paper plant's bottom ash regeneration manufacture at biomass fuel technique | |
CN206927865U (en) | RDF manufacturing systems based on high-pressure extrusion isolation technics | |
CN103785670A (en) | Method for harmless treatment of waste residue in paper making | |
CN204263405U (en) | A kind of waste household appliances plastic casing treatment system | |
CN115787331A (en) | Preparation method of full straw biochemical mechanical pulp | |
CN210253504U (en) | Garbage sorting system | |
CN105363765B (en) | A kind of life refuse processing method | |
CN108589362B (en) | A kind of dry isolated method of waste and old paper composite wallpaper | |
CN209810903U (en) | Coarse slag crushing device system in waste paper regeneration process | |
CN107321763B (en) | A kind of house refuse multistage recovery and treatment method | |
CN102816248A (en) | Dry type cassava starch extraction process | |
CN113234469A (en) | Low-value waste plastic dry pretreatment system and method based on pyrolysis oil production | |
CN103521505A (en) | Method for production of plate from light garbage | |
CN107175252B (en) | The processing method and its device and product of a kind of aluminium waste water slag and application | |
CN111361056A (en) | Process for recycling papermaking waste residues | |
CN105235099A (en) | Method for machining spinning fibrous materials with abandoned plastic bottles as basic materials | |
CN101736635B (en) | Magnetic separation and deinking method for waste paper |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
RJ01 | Rejection of invention patent application after publication | ||
RJ01 | Rejection of invention patent application after publication |
Application publication date: 20191011 |